WO2019053861A1 - Électrode et pile à électrolyte non aqueux - Google Patents

Électrode et pile à électrolyte non aqueux Download PDF

Info

Publication number
WO2019053861A1
WO2019053861A1 PCT/JP2017/033336 JP2017033336W WO2019053861A1 WO 2019053861 A1 WO2019053861 A1 WO 2019053861A1 JP 2017033336 W JP2017033336 W JP 2017033336W WO 2019053861 A1 WO2019053861 A1 WO 2019053861A1
Authority
WO
WIPO (PCT)
Prior art keywords
particles
electrode
carbon material
less
mixture layer
Prior art date
Application number
PCT/JP2017/033336
Other languages
English (en)
Japanese (ja)
Inventor
祐輝 渡邉
大 山本
駿忠 中澤
哲郎 鹿野
政典 田中
Original Assignee
株式会社 東芝
東芝インフラシステムズ株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 株式会社 東芝, 東芝インフラシステムズ株式会社 filed Critical 株式会社 東芝
Priority to JP2019541582A priority Critical patent/JP6952784B2/ja
Priority to EP17924977.6A priority patent/EP3683865B1/fr
Priority to PCT/JP2017/033336 priority patent/WO2019053861A1/fr
Priority to CN201780094329.0A priority patent/CN111052455B/zh
Publication of WO2019053861A1 publication Critical patent/WO2019053861A1/fr
Priority to US16/806,005 priority patent/US11967720B2/en

Links

Images

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/0402—Methods of deposition of the material
    • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/043—Processes of manufacture in general involving compressing or compaction
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • H01M4/1391—Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/364—Composites as mixtures
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624—Electric conductive fillers
    • H01M4/625—Carbon or graphite
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/021—Physical characteristics, e.g. porosity, surface area
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027—Negative electrodes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028—Positive electrodes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

Definitions

  • Embodiments of the present invention relate to an electrode and a non-aqueous electrolyte battery.
  • An object of the present invention is to provide an electrode capable of realizing a non-aqueous electrolyte battery capable of exhibiting excellent output performance, and a non-aqueous electrolyte battery provided with the electrode.
  • an electrode is provided.
  • the electrode includes an electrode mixture layer containing an active material and a conductive aid.
  • the electrode mixture layer satisfies a ratio P1 / P2 within the range of 2 to less than 8 and a ratio S1 / S2 within the range of 3 to less than 10 in the log differential pore volume distribution by mercury porosimetry.
  • P1 is a value [mL / g] of the maximum log differential pore volume in a pore diameter range of 0.1 ⁇ m to 1 ⁇ m in the log differential pore volume distribution of the electrode mixture layer
  • P2 is It is a value [mL / g] of log differential pore volume about a 0.03 micrometer pore diameter in log differential pore volume distribution of an electrode mixture layer
  • S1 is an integral value within the pore diameter range of 0.1 ⁇ m or more and 1 ⁇ m or less in the log differential pore volume distribution of the electrode mixture layer
  • S2 is from 0 ⁇ m in the log differential pore volume distribution of the electrode mixture layer It is an integral value in the range of a pore diameter of less than 0.1 ⁇ m.
  • a non-aqueous electrolyte battery comprises an electrode according to the first embodiment as a positive electrode, a negative electrode, and a non-aqueous electrolyte.
  • FIG. 1 is a schematic cross-sectional view of an example of an electrode according to a first embodiment.
  • FIG. 2 is a Raman spectrum of the graphite which the electrode mixture layer which the electrode of an example concerning a 1st embodiment comprises comprises.
  • FIG. 3 is a Raman spectrum of carbon black which the electrode mixture layer which the electrode of an example concerning a 1st embodiment comprises comprises.
  • FIG. 4 is a log differential pore volume distribution of the electrode mixture layer which the electrode of an example concerning a 1st embodiment comprises.
  • FIG. 5 is an SEM image of an example of particles of the first carbon material.
  • FIG. 6 is a schematic cutaway perspective view of a first example nonaqueous electrolyte battery according to a second embodiment.
  • 7 is a schematic enlarged cross-sectional view of a portion A of FIG.
  • FIG. 8 is a schematic cutaway perspective view of a non-aqueous electrolyte battery of a second example according to the second embodiment.
  • an electrode is provided.
  • the electrode includes an electrode mixture layer containing an active material and a conductive aid.
  • the electrode mixture layer satisfies a ratio P1 / P2 within the range of 2 to less than 8 and a ratio S1 / S2 within the range of 3 to less than 10 in the log differential pore volume distribution by mercury porosimetry.
  • P1 is a value [mL / g] of the maximum log differential pore volume in a pore diameter range of 0.1 ⁇ m to 1 ⁇ m in the log differential pore volume distribution of the electrode mixture layer
  • P2 is It is a value [mL / g] of log differential pore volume about a 0.03 micrometer pore diameter in log differential pore volume distribution of an electrode mixture layer
  • S1 is an integral value within the pore diameter range of 0.1 ⁇ m or more and 1 ⁇ m or less in the log differential pore volume distribution of the electrode mixture layer
  • S2 is from 0 ⁇ m in the log differential pore volume distribution of the electrode mixture layer It is an integral value in the range of a pore diameter of less than 0.1 ⁇ m.
  • adjusting the porosity of the electrode mixture layer can be mentioned using a combination of several types of conductive support agents.
  • a plurality of types of conductive aids having different particle sizes an arrangement can be achieved to fill the voids between active material particles, thereby forming a good conductive path and providing excellent output performance. Can be expected to be realized.
  • the inventors of the present invention found that the conductive aid is contained in a mixed state in the aggregated state even if it is contained in a relatively large amount relative to the weight of the active material. It has been found that excellent output performance can not be exhibited. And, a carbon material widely used as a conductive aid has a property of being easily aggregated, and therefore, when a plurality of kinds of conductive aids are simply included in the electrode mixture layer, the aggregation of the conductive aid occurs. It turned out that the effect of each conductive support agent can not be exhibited.
  • the paint was prepared by dispersing the conductive aid so as not to aggregate, it was found that a particularly strong shearing force is applied to the conductive aid having a small particle diameter. And, in an electrode mixture layer produced using a paint prepared by such dispersion, the pore diameter becomes extremely small, and such an electrode mixture layer is hard to be impregnated with the non-aqueous electrolyte, It turned out that the diffusivity of Li ion worsens and it is not possible to realize excellent output performance. Furthermore, the conductive aid to which a strong shear force is applied reduces the crystallinity of the surface layer and reduces the conductivity, and the electrode mixture layer containing such a conductive aid exhibits excellent output performance. It turns out that you can not do it.
  • Such a device includes, for example, preparing a paint containing a conductive aid in a method including strong dispersion.
  • a strong shearing force is added to the conductive aid to lower the crystallinity of the surface layer of the conductive aid, and in such a device, the conductive aid It turned out that the original excellent output performance can not be exhibited.
  • the electrode mixture layer obtained by such a device has extremely small pore diameter due to the strong shear force applied to the conductive additive, and can not exhibit excellent output performance. .
  • the inventors achieved the electrode according to the first embodiment as a result of intensive research based on the above findings.
  • the electrode according to the first embodiment can realize a nonaqueous electrolyte battery capable of exhibiting excellent output performance, for the reasons described below.
  • P1 is a value [mL / g] of the maximum log differential pore volume in a pore diameter range of 0.1 to 1 ⁇ m in the log differential pore volume distribution of the electrode mixture layer
  • P2 is It is a value [mL / g] of log differential pore volume about a 0.03 micrometer pore diameter in the differential pore volume distribution of an electrode mixture layer.
  • S1 is an integral value within the pore diameter range of 0.1 ⁇ m or more and 1 ⁇ m or less in the log differential pore volume distribution of the electrode mixture layer
  • S2 is the log differential pore volume distribution of the electrode mixture layer It is an integral value in the pore diameter range of more than 0 ⁇ m and less than 0.1 ⁇ m.
  • the conductive aid is dispersed sufficiently uniformly, and the conductive aid sufficiently fills the voids between the active materials. It can be said that there are too few pores that inhibit the diffusion of Li ions.
  • the electrode mixture layer in such a state can realize excellent output performance.
  • the electrode according to the first embodiment can realize a nonaqueous electrolyte battery that can exhibit excellent output performance.
  • the proportion of pores having a pore diameter of 0.03 ⁇ m or less is too large.
  • the proportion of pores having a pore diameter of less than 0.1 ⁇ m is too large.
  • the proportion of pores having a pore diameter of 0.03 ⁇ m is too large.
  • the conductive aid is not uniformly dispersed in the electrode mixture layer.
  • Such an electrode mixture layer can not achieve excellent output performance because current distribution can be biased when a large current flows.
  • the conductive aid preferably includes particles of the first carbon material and particles of the second carbon material. Moreover, it is preferable that ratio d1 / d2 of an average particle diameter exists in the range of 2 or more and 14 or less.
  • d1 is the average particle size of the particles of the first carbon material
  • d2 is the average particle size of the particles of the second carbon material.
  • the particles of the first carbon material preferably satisfy the intensity ratio G 1 / D 1 in the range of 2 or more and less than 4 in the Raman spectrum of the electrode mixture layer.
  • G 1 in the Raman spectrum of the electrode mixture layer, the intensity in G 1 band peak top appears in the region of 1550cm -1 ⁇ 1650cm -1.
  • D 1 is the Raman spectrum of the electrode mixture layer, the intensity of the D 1 band peak top appears in the region of 1300cm -1 ⁇ 1400cm -1.
  • the G 1 band and the D 1 band appear in the same Raman spectrum, and the unit of intensity is an arbitrary unit.
  • Such particles of the first carbon material can exhibit excellent crystallinity on the surface, and can form an excellent conductive path.
  • the particles of the first carbon material are flat particles, and the aspect ratio thereof is preferably in the range of 1.5 or more and 2 or less.
  • the particles of the first carbon material of this preferred embodiment have a sufficient anisotropy so that they have a spherical or cubic shape.
  • Such particles of the first carbon material are, for example, other carbon materials dispersed together during preparation of a paint for electrode preparation, specifically, a second particle having a smaller average particle size than the first carbon material.
  • the particles of the carbon material of the present invention can be protected from the shear force while preventing the reduction of the crystallinity of the surface of the particles of the first carbon material and the crystallinity of the surface of the particles of the second carbon material.
  • the particles of the second carbon material preferably satisfy the intensity ratio G 2 / D 2 within the range of 1 or more and less than 1.5 in the Raman spectrum of the electrode mixture layer.
  • G 2 in the Raman spectrum of the electrode mixture layer, the intensity of the G 2 bands peak top appears in the region of 1550cm -1 ⁇ 1650cm -1.
  • D 2 is the Raman spectrum of the electrode mixture layer, the intensity of the D 2 band peak top appears in the region of 1300cm -1 ⁇ 1400cm -1.
  • the G 2 band and the D 2 band appear in the same Raman spectrum, and the unit of intensity is an arbitrary unit.
  • Such particles of the second carbon material can have an average particle size smaller than that of the particles of the first carbon material, although the crystallinity of the surface is lower than that of the particles of the first carbon material.
  • the particles of the second carbon material may form an excellent conductive network if they are sufficiently uniformly dispersed in the electrode mixture layer in the state of secondary particles in which several tens of primary particles are aggregated. it can.
  • the particles of the second carbon material have a small average particle diameter, hydrophobic interaction is strongly expressed, and secondary particles formed by aggregation of several hundreds of primary particles tend to be formed.
  • the particles of the second carbon material can not be dispersed uniformly.
  • a conductive network is formed where a large amount of the second carbon material is present, but a portion with a small amount of the second carbon material is electrically isolated.
  • the shearing force is applied too strongly to the particles of the second carbon material, less than 10 primary particles constituting the secondary particles of the particles of the second carbon material turn into.
  • An electrode mixture layer produced using a paint containing particles of such a second carbon material can form an excellent conductive network even if the dispersibility of the particles of the second carbon material is high. Can not.
  • the particles of the second carbon material are suitable secondary particles. While maintaining the state, it may be in a sufficiently uniformly dispersed state in the electrode mixture layer. Therefore, the particles of the second carbon material contained in the electrode mixture layer of the electrode of this aspect can form a more excellent conductive network.
  • the weight ratio C1 / C2 is preferably in the range of 0.2 or more and less than 1.
  • C1 is the weight of the particles of the first carbon material contained in the electrode mixture layer
  • C2 is the weight of the particles of the second carbon material contained in the electrode mixture layer. That is, in the electrode mixture layer, the content of the particles of the second carbon material is preferably larger than the content of the particles of the first carbon material.
  • the particles of the first carbon material can be dispersed even if a strong shear force is applied.
  • the particles of the second carbon material can be protected.
  • the particles of the first carbon material of the preferred embodiment have an aspect ratio of 2 or less, the shape is not easily broken even if a strong shear is applied during the preparation of the paint. This is also the reason why the particles of the first carbon material can sufficiently protect the particles of the second carbon material.
  • the crystallinity of the surface layer of the particles of the second carbon material can be maintained high. It is possible to prepare a paint for electrode preparation by preventing aggregation of the particles of the carbon material and the particles of the second carbon material. Further, by using the paint prepared in this manner, it is possible to prevent the pore diameter from becoming extremely small in the electrode mixture layer.
  • the particles of the first carbon material and the particles of the second carbon material having different average particle sizes make the gaps between the active materials more than the case of using only the particles of the conductive aid of the same particle size. It can be filled enough.
  • the electrode according to the first embodiment may be, for example, a positive electrode used in a non-aqueous electrolyte battery, or may be a negative electrode.
  • the electrode according to the first embodiment includes an electrode mixture layer.
  • the electrode mixture layer contains an active material and a conductive aid.
  • the electrode according to the first embodiment can further include a current collector.
  • the electrode mixture layer can be formed on the current collector.
  • the active material may be, for example, a positive electrode active material.
  • the positive electrode active material is not particularly limited.
  • Examples of the positive electrode active material nickel-cobalt-manganese composite oxide (NCM: e.g., Li a Ni 1-xy Co x Mn y O 2 ( subscripts x and y, 0 ⁇ x ⁇ 0.4 and 0 ⁇ y ⁇ Fills 0.35, and the subscript a is in the range of 0.9 ⁇ a ⁇ 1.2)), lithium manganese complex oxide (LMO: for example, Li b Mn 2 O 4 or Li c MnO 2 (subscript) b is in the range of 0.9 ⁇ b ⁇ 1.2, and the subscript c is in the range of 0.9 ⁇ c ⁇ 1.2)), lithium nickel composite oxide (eg Li d NiO 2) (Subscript d is in the range of 0.9 ⁇ d ⁇ 1.2), lithium cobalt composite oxide (LCO: for example, Li
  • the content is preferably 70% by weight or more and 100% by weight or less based on the weight of the positive electrode active material.
  • the active material as the positive electrode active material may have, for example, a particle shape.
  • the particles of the positive electrode active material are preferably secondary particles formed by aggregation of primary particles.
  • the particles of the positive electrode active material are secondary particles having an average secondary particle diameter of not less than 3 ⁇ m and less than 10 ⁇ m, which are formed by aggregation of primary particles having an average primary particle diameter of not less than 0.1 ⁇ m and less than 1 ⁇ m. preferable.
  • the positive electrode active material particles having an average primary particle size and an average secondary particle size in this range can enhance the diffusion of lithium ions in the electrode mixture layer, and form a conductive network even with a small amount of conductive additive be able to.
  • the active material may be a negative electrode active material.
  • the negative electrode active material can include, for example, one or more negative electrode active materials.
  • the negative electrode active material for example, metals, metal alloys, metal oxides, metal sulfides, metal nitrides, and the like can be used.
  • the metal oxide for example, a substance containing titanium, such as titanium oxide, lithium titanium composite oxide, and niobium titanium composite oxide, and niobium composite oxide can be used.
  • metal sulfides include titanium sulfides such as TiS 2 , molybdenum sulfides such as MoS 2 , iron sulfides such as FeS, FeS 2 and LixFeS 2 .
  • the active material as the negative electrode active material may be, for example, in the form of particles.
  • the particles of the negative electrode active material are preferably secondary particles formed by aggregation of primary particles.
  • the particles of the negative electrode active material are secondary particles formed by aggregation of primary particles having an average primary particle diameter of 0.1 ⁇ m or more and less than 0.5 ⁇ m and having an average secondary particle diameter of 0.6 ⁇ m or more and less than 2 ⁇ m. It is further preferred that
  • the conductive aid preferably includes the particles of the first carbon material and the particles of the second carbon material described above.
  • Examples of particles of the first carbon material may include, for example, particles of graphite, particles of graphene and particles of carbon fibers.
  • the particles of the first carbon material can include, for example, at least one particle selected from the group consisting of particles of graphite, particles of graphene, and particles of carbon fibers.
  • one carbon fiber particle refers to one carbon fiber.
  • the particles of the first carbon material are preferably flat particles having an aspect ratio in the range of 1.5 or more and 2 or less, as described above.
  • the aspect ratio of the particles is the ratio of the largest length (long diameter) of the particles to the smallest length (short diameter) in the direction perpendicular to the long diameter of the particles.
  • the aspect ratio of the particles of the first carbon material is preferably in the range of 1.6 or more and 1.8 or less, and more preferably in the range of 1.7 or more and 1.8 or less.
  • Examples of the particles of the second carbon material include particles of carbon black.
  • Examples of carbon black include, for example, acetylene black, ketjen black, furnace black, channel black, lamp black and thermal black.
  • the G 1 band for the particles of the first carbon material and the G 2 band for the particles of the second carbon material can appear at the same position in the Raman spectrum.
  • each band is distinguished by performing multivariate analysis using the intensity ratio G / D obtained from the Raman spectrum of each of the first carbon material and the second carbon material. be able to.
  • a similar distinction can be made between the D 1 band for the particles of the first carbon material and the D 2 band for the particles of the second carbon material.
  • the strength ratio G 1 / D 1 is more preferably 2.2 or more and 3.5 or less, and still more preferably 2.2 or more and 3 or less.
  • the strength ratio G 2 / D 2 is more preferably 1.1 or more and 1.4 or less, and still more preferably 1.2 or more and 1.3 or less.
  • the strength ratio G 1 / D 1 of the particles of the first carbon material is different depending on, for example, the preparation conditions of the electrode, particularly the preparation conditions of the paint for electrode preparation, even if the particles of the same first carbon material are used It is possible.
  • the intensity ratio G 1 / D 1 of the particles of the first carbon material contained in the electrode according to the first embodiment is an intensity ratio of the electrode mixture layer measured by Raman spectroscopy.
  • the strength ratio G 2 / D 2 of the second carbon material may differ depending on, for example, the preparation conditions of the electrode, particularly the preparation conditions of the paint for electrode preparation, even if particles of the same second carbon material are used. There is a possibility.
  • the intensity ratio G 2 / D 2 of the second carbon material contained in the electrode according to the second embodiment is an intensity ratio obtained by measuring the electrode mixture layer by Raman spectroscopy.
  • the strength ratio G 1 / D 1 of the particles of the first carbon material as the raw material is preferably in the range of 3 or more and 10 or less, and more preferably in the range of 5 or more and 10 or less. Further, the strength ratio G 2 / D 2 of the particles of the second carbon material as the raw material is preferably in the range of 1.2 or more and less than 2, and is in the range of 1.5 or more and less than 2 More preferable.
  • the ratio d1 / d2 of the average particle diameter of the conductive additive in the electrode mixture layer is preferably in the range of 4 or more and 14 or less, and more preferably in the range of 8 or more and 14 or less.
  • the ratio d1 / d2 is in these ranges, the effect of protecting the particles of the second carbon material by the particles of the first carbon material can be further enhanced.
  • the average particle diameter d1 of the particles of the first carbon material is preferably in the range of 4 ⁇ m to less than 7 ⁇ m. When the average particle diameter d1 of the particles of the first carbon material is in this range, a small amount of conductive network can be formed in the electrode mixture layer.
  • the average particle diameter d1 is more preferably in the range of 4 or more and 6 or less.
  • the average particle diameter d2 of the particles of the second carbon material is preferably in the range of 0.5 ⁇ m or more and less than 2 ⁇ m.
  • the particles of the second carbon material in which the average particle diameter d2 of the particles of the second carbon material is in this range, when used in combination with the particles of the first carbon material, are arranged to fill voids in the electrode mixture layer It can be done to provide a good conducting network.
  • the average particle diameter d2 is more preferably in the range of 0.5 or more and 1 or less.
  • the weight ratio C1 / C2 of the conductive aid in the electrode mixture layer is more preferably in the range of 0.3 or more and less than 1, and still more preferably in the range of 0.3 or more and 0.7 or less. It is particularly preferable to be in the range of 0.4 or more and 0.7 or less. When the ratio C1 / C2 is in these ranges, the effect of protecting the particles of the second carbon material by the particles of the first carbon material can be further enhanced.
  • the area ratio A2 / A1 in the electrode mixture layer is preferably in the range of 0.1 or more and 0.4 or less.
  • A1 is the area [ ⁇ m] of the active material contained in 1 ⁇ m 2 of the cross section of the electrode mixture layer
  • a 2 is the area of the conductive additive contained in 1 ⁇ m 2 of the cross section of the electrode mixture layer [ ⁇ m].
  • An electrode having an area ratio A2 / A1 in the above range can realize an excellent balance between energy density and output performance.
  • the area ratio A2 / A1 is more preferably in the range of 0.15 or more and 0.3 or less.
  • the electrode according to the first embodiment is a positive electrode, and the area ratio A2 / A1 is 0.15 or more and 0.3 or less. In another aspect, for example, the electrode according to the first embodiment is a negative electrode, and the area ratio A2 / A1 is 0.1 or more and 0.2.
  • the electrode mixture layer can further include a binder.
  • the binder can exhibit the function of bonding the active material and the current collector.
  • the binder include, for example, polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVdF), fluorocarbon rubber, styrene-butadiene rubber (SBR), polypropylene (PP), polyethylene (PE), and acrylic copolymer.
  • the main component is a binder, and carboxymethylcellulose (CMC).
  • the proportions of the active material, the conductive additive and the binder in the electrode mixture layer are 70% by weight or more and 96% by weight or less, 1% by weight or more and 20% by weight or less, and 1% by weight or more and 10% by weight
  • the content is preferably 90% by weight or more and 95% by weight or less, 3% by weight or more and 7% by weight or less, and more preferably 1% by weight or more and 5% by weight or less.
  • the electrode according to the first embodiment is a positive electrode and in the electrode mixture layer
  • the proportions of the active material, the conductive additive and the binder are 70% by weight or more and 95% by weight or less, 1% by weight or more and 20% by weight or less, and 1% by weight or more and 10% by weight or less.
  • the electrode according to the first embodiment is a negative electrode
  • the proportions of the active material, the conductive additive, and the binder in the electrode mixture layer are 70% by weight or more and 96% by weight or less, respectively. 2% by weight or more and 20% by weight or less, and 2% by weight or more and 10% by weight or less.
  • the ratio P1 / P2 is preferably in the range of 4 or more and 8 or less.
  • the conductive aid may be dispersed more uniformly, and the conductive aid may be in a state in which the voids between the active materials are more fully filled.
  • the ratio P1 / P2 is more preferably 4 or more and 7 or less.
  • the ratio S1 / S2 is preferably in the range of 3.5 or more and 7 or less.
  • An electrode having a ratio S1 / S2 in this range may be in a state of having too few small pores that inhibit the diffusion of Li ions.
  • the ratio S1 / S2 is more preferably 3.5 or more and 6 or less.
  • the current collector can have, for example, a strip-like planar shape.
  • the strip-shaped current collector can have two surfaces including a first surface and a second surface as its back surface.
  • the electrode mixture layer can be formed on both surfaces and one surface of the current collector.
  • the current collector can also include a portion not carrying the electrode mixture layer on the surface. This part can, for example, act as a current collection tab.
  • a sheet containing a material with high electrical conductivity can be used as the current collector of the positive electrode.
  • an aluminum foil or an aluminum alloy foil can be used as the positive electrode current collector.
  • its thickness is, for example, 20 ⁇ m or less, preferably 15 ⁇ m or less.
  • the aluminum alloy foil can include magnesium, zinc, silicon and the like.
  • content of transition metals, such as iron, copper, nickel, and chromium, contained in aluminum alloy foil is 1% or less.
  • the current collector of the negative electrode a sheet containing a material having high electrical conductivity and capable of suppressing corrosion in the working potential range of the negative electrode can be used.
  • the negative electrode current collector the same aluminum foil or aluminum alloy foil as that which can be used as the positive electrode current collector can be used.
  • Electrode incorporated in the non-aqueous electrolyte battery is pretreated in the following procedure. First, the non-aqueous electrolyte battery is disassembled in a glove box filled with argon, and the electrode to be measured is taken out from the non-aqueous electrolyte battery. The removed electrode is then washed with methyl ethyl carbonate (MEC). The washed electrode is then dried under an atmosphere of 100 ° C. and a gauge pressure of ⁇ 75 kPa. The dried electrode is subjected to each analysis described below. Hereinafter, the electrode to be measured is simply referred to as "electrode".
  • MEC methyl ethyl carbonate
  • the aspect ratio of the conductive additive can be measured by the following procedure. First, the electrode is polished perpendicular to the current collector. Next, a cross section of the polished electrode is photographed using a transmission electron microscope (TEM) or a scanning electron microscope (SEM). Analyze the image of the picture taken and select 50 particles of conductive aid. The major axes of the cross-sections of the 50 selected conductive auxiliary particles are measured. In addition, the minor diameter (the thickness of the particles) of the cross section of the 50 particles of the conductive support agent, which is the same as that measured when the major diameter is determined, is measured.
  • TEM transmission electron microscope
  • SEM scanning electron microscope
  • the average value is determined for each of the measured major axis and minor axis, and the ratio of the average major axis to the average minor axis is taken as the aspect ratio (major axis / minor axis).
  • the particles to be measured here are limited to those perpendicular to the c-axis direction. It can be confirmed by observing the atomic arrangement whether it is oriented perpendicularly to the c-axis direction. Particles perpendicular to the c-axis direction can be observed from directly above the flat surface of the particles, and the aspect ratio can be accurately obtained.
  • the particles used for measurement are limited to those having a major axis of 3 ⁇ m or more. If the major axis is less than 3 ⁇ m, the crystal is likely to be broken in the manufacturing process, and therefore, it is not suitable for measuring the aspect ratio.
  • Whether the particles whose major and minor axes are measured are particles of the first carbon material or particles of the second carbon material can be determined by the G / D ratio in the Raman spectrum.
  • Shimadzu Autopore 9520 (Autopore 9520 model manufactured by Shimadzu Corporation) is used.
  • an electrode cut into a size of about 25 ⁇ 25 mm 2 is used.
  • This sample is folded and taken into the measurement cell, and the initial pressure is 20 kPa (the initial pressure 20 kPa corresponds to about 3 psia and the pore pressure corresponds to the pressure applied to the sample of about 60 ⁇ m) and the maximum pressure 414 Mpa (the maximum pressure 414 Mpa is about It corresponds to 59986 psia, and corresponds to the pressure applied to the sample having a pore diameter of about 0.003 ⁇ m.
  • the average value of three samples is used as the measurement result.
  • the pore specific surface area is calculated as the pore shape is cylindrical.
  • P is the pressure to be applied
  • D is the pore diameter
  • ⁇ is the surface tension of mercury (480 dyne ⁇ cm ⁇ 1 )
  • ⁇ 140 ° in the contact angle between mercury and the pore wall surface. Since ⁇ and ⁇ are constants, the relationship between the applied pressure P and the pore diameter D can be obtained from the Washburn equation, and the pore diameter and its volume distribution can be derived by measuring the mercury intrusion volume at that time. Can.
  • the electrode surface is divided into 1024 regions each having a size of 40 ⁇ 40 ⁇ m.
  • Raman spectroscopy is performed for each point to obtain a Raman spectrum.
  • the Raman spectra can be mapped with a plurality of different Raman spectra corresponding to the respective materials. By this separation by mapping, it is possible to separate the Raman spectrum of the particles of the first carbon material and the Raman spectrum of the particles of the second carbon material from each other.
  • the intensity ratio G 1 / D 1 of the G 1 band to the D 1 band is the ratio of the peak top intensity of the G 1 band to the peak top intensity of the D 1 band.
  • the intensity ratio G 2 / D 2 of the G 2 band to the D 2 band is the ratio of the peak top intensity of the G 2 band to the peak top intensity of the D 2 band.
  • Raman mapping can be performed on the constituent materials of
  • Raman mapping can be obtained for the electrode mixture layer, which indicates how and how substances are arranged on the surface of the electrode mixture layer.
  • the electrode is polished perpendicular to the current collector.
  • the cross section of the polished electrode is photographed.
  • the image of the photographed picture is analyzed to select 50 particles of the conductive auxiliary agent contained in the electrode mixture layer.
  • the major axes of the cross-sections of the 50 selected conductive auxiliary particles are measured.
  • the cross-sectional photograph of an electrode is generally image
  • SEM scanning Electron Microscope
  • a cross-sectional photograph may be taken in the same manner as described above using a polarization microscope or a transmission electron microscope.
  • the particles to be measured here are limited to those perpendicular to the c-axis direction.
  • Whether the particle whose major axis has been measured is a particle of the first carbon material or a particle of the second carbon material can be determined by the G / D ratio in the Raman spectrum.
  • the average value of the measurement results for the particles of the first carbon material is taken as the average particle diameter d1 of the first carbon material. Further, an average value of measurement results of particles of the second carbon material is taken as an average particle diameter d2 of the second carbon material.
  • average particle size in the present specification is an average (number average) value of particle sizes measured without distinction between primary particles and secondary particles.
  • TG / DTA7200 manufactured by SII Nano Technology Co., Ltd. can be used as the measurement device.
  • a small electrode is cut out to prepare a measurement sample. For example, let 10 ⁇ 1 mg as a standard, and use it as a measurement sample.
  • the obtained sample is placed in a platinum PAN (measurement container) having a diameter of 5 mm, and this is set on a measurement table.
  • the measurement is performed by changing the temperature of the sample as follows. First, the temperature is raised from room temperature to 500 ° C. in a nitrogen atmosphere. Then, the temperature is once lowered to 300 ° C. Then, the atmosphere is switched to air and the temperature is raised again to 800.degree. The temperature raising time and the temperature lowering rate are both 5 ° C. per minute. In these temperature changes, the weight loss Tc2 obtained at 600 ° C. to 700 ° C.
  • the weight ratio C1 / C2 can be calculated by calculating the ratio Tc1 / Tc2.
  • the flow rate of the gas is 200 ml / min for both nitrogen and the atmosphere.
  • Electrode incorporated in the non-aqueous electrolyte battery is pretreated in the following procedure. First, the non-aqueous electrolyte battery is disassembled in a glove box filled with argon, and the electrode to be measured is taken out from the non-aqueous electrolyte battery. The removed electrode is then washed with methyl ethyl carbonate (MEC). The washed electrode is then dried under an atmosphere of 100 ° C. and a gauge pressure of ⁇ 75 kPa. The dried electrode is subjected to each analysis described below. Hereinafter, the electrode to be measured is simply referred to as "electrode".
  • MEC methyl ethyl carbonate
  • G-2 Measurement of Area Ratio A2 / A1
  • the measurement of the area ratio A2 / A1 can be carried out according to the following procedure. First, the electrode is polished perpendicular to the current collector. Next, the cross section of the polished electrode is photographed using a scanning electron microscope (SEM). At this time, the field of view is adjusted to be 30 ⁇ m square. Then, EDX analysis is performed on the obtained visual field. At this time, mapping is performed with the elements Ni, Co, Mn, Fe and Ti, and the total area of the obtained regions is A1. However, in the area where two or more types of multiple elements overlap, only one type of area is counted.
  • SEM scanning electron microscope
  • LiNi 1/3 Co 1/3 Mn 1/3 O 2 is mapped in the same region with three elements of Ni, Co and Mn, in which case one of Ni, Co or Mn Only record the minutes. Similarly, mapping is performed with the element C, and the area of the obtained region is A2. Thereby, the area ratio A2 / A1 of the conductive additive and the active material in the cross section of the electrode mixture layer can be calculated.
  • FIG. 1 is a schematic cross-sectional view of an example of an electrode according to a first embodiment.
  • An electrode 10 shown in FIG. 1 includes a strip-shaped current collector 11 and an electrode mixture layer 12 formed on both surfaces of the current collector.
  • the surface 12 a of the electrode mixture layer 12 is the surface of the electrode 10.
  • the electrode mixture layer 12 contains an active material and a conductive additive.
  • the conductive aid includes particles of graphite as particles of the first carbon material and particles of carbon black as particles of the second carbon material.
  • the ratio d1 / d2 of the average particle size is 8, and the weight ratio C1 / C2 is 0.6.
  • FIG. 2 is a Raman spectrum of particles of graphite as particles of the first carbon material contained in the electrode mixture layer 12. Raman spectra shown in FIG. 2, it has a G 1 band having a peak top in 1590 cm -1, having a D 1 band having a peak top in the 1350 cm -1. Also, the intensity ratio G 1 / D 1 is 2.3.
  • FIG. 3 is a Raman spectrum of particles of carbon black as particles of the second carbon material contained in the electrode mixture layer 12.
  • Raman spectra shown in FIG. 3 has a G 2 band having a peak top in 1350 cm -1, with a D 2 band having the peak top at 1590 cm -1.
  • the intensity ratio G 2 / D 2 is 1.1.
  • FIG. 4 is a Log differential pore volume distribution for the electrode mixture layer 12 shown in FIG.
  • the ratio P1 / P2 is 5.9 and the ratio S1 / S2 is 9.5.
  • the pore diameter taking a value of the largest log differential pore volume in the pore diameter range of 0.1 ⁇ m to 1 ⁇ m was 0.25 ⁇ m.
  • FIG. 5 is a cross-sectional SEM image including one particle of graphite for the electrode mixture layer 12 shown in FIG.
  • This image is one SEM image of a cross section obtained by polishing the electrode mixture layer 12 parallel to the current collector 11. It was 1.8 when the aspect-ratio of the particle
  • the electrode according to the first embodiment is prepared, for example, by using the conductive aid of the preferred embodiment described above and, for example, as described in the example of the manufacturing method described below, preparation of a paint for electrode preparation In the process, dispersion is carried out by applying strong shear force.
  • the electrode according to the first embodiment can not be realized simply by using the mixture of the particles of the first carbon material and the particles of the second carbon material described above.
  • the method of manufacturing the electrode according to the first embodiment is not limited to the examples shown below.
  • particles of the first carbon material and particles of the second carbon material are prepared. Next, these are each measured so that the weight ratio C1 / C2 described above is in the range of 0.2 or more and less than 1, and mixed to obtain a mixture.
  • the mixture is dispersed, for example, with a Henschel mixer. This dispersion is called pre-dispersion of the conductive aid.
  • Such pre-dispersion of the conductive aid can increase the probability that particles of the first carbon material will be present to protect around each of the particles of the second carbon material.
  • the mixture obtained by pre-dispersion is poured into a solvent such as N-methylpyrrolidone to obtain a dispersion.
  • the dispersion is stirred.
  • “Neritsutaro” manufactured by Shinky Co., Ltd. can be used.
  • the binder is added to the dispersion.
  • the binder is divided into a plurality of times and added in a substantially equal amount.
  • the dispersion is stirred. Cohesion of the conductive aid can be prevented by the addition of the binder divided into multiple times.
  • the active material is added to the dispersion.
  • the dispersion is then adjusted to a solids content in the range of 65% to 85% by adding a solvent, such as N-methyl pyrrolidone.
  • a solvent such as N-methyl pyrrolidone.
  • the solids content is adjusted within the range of 70% to 80%.
  • the dispersion thus obtained is then stirred several more times. After each round of stirring, it is cooled, for example for 10 minutes at room temperature. Thereby, aggregation of the conductive aid can be loosened while suppressing the decrease in crystallinity of the active material.
  • the further stirring here is preferably performed three or more times, and more preferably five times or more.
  • a high shear force can be applied to the dispersion by stirring a plurality of times in a state in which the solid content is high. Thereby, the active material and the conductive additive in the dispersion can be uniformly dispersed.
  • the multiple stirring is called "solid mixing".
  • the particles of the first carbon material are hard
  • the particles of the second carbon material can be protected from the strong shear force in That is, according to the method shown here as an example, the active material and the conductive aid can be uniformly dispersed while preventing the decrease in the crystallinity of the surface layer of the second carbon material contained in the conductive aid.
  • an NMP solvent is added in two or three portions to the mixture obtained by solid kneading, and the solid content in the mixture is adjusted to be in the range of 55% to 65%.
  • a shear force is applied to the solid content-adjusted mixture using a medium-free high pressure dispersing device (medialess high pressure dispersing device).
  • a medium-free high pressure dispersing device for example, a jet mill, a film mix, a jet paster, etc. may be mentioned.
  • the processing capacity is preferably in the range of 0.5 to 2 kg / hr.
  • the jet mill can crush large aggregates without reducing the crystallinity of the active material and the conductive aid because of the crush principle using only compressed air.
  • a shear force is further applied to the mixture supplied to the medialess high pressure dispersing device using a dispersing device using media.
  • a dispersion apparatus using media a bead mill, a ball mill and the like can be mentioned.
  • zirconia beads of ⁇ 0.5 to 1 mm as the beads.
  • the dispersibility of the active material and the conductive additive in the mixture can be further improved.
  • the improved dispersibility can be maintained also in the electrode mixture layer produced using this mixture as a paint.
  • the media diameter is preferably in the range of ⁇ 0.5 to 1 mm so that the energy at the time of collision becomes small. Also, in order to reduce the frequency of collisions, it is preferable to set the filling rate of the media as low as 40 to 50%.
  • the coating for producing the electrode mixture layer can be obtained by the dispersing device using the media described above.
  • the electrode according to the first embodiment can be obtained which exhibits the log differential pore volume distribution described above.
  • an electrode is provided.
  • the electrode includes an electrode mixture layer containing an active material and a conductive aid.
  • the electrode mixture layer has a ratio P1 / P2 within the range of 2 to less than 8 and a ratio S1 / 1 within the range of 3 to less than 10 in the log differential pore volume distribution of the electrode mixture layer by mercury porosimetry. Meet S2.
  • the conductive aid is sufficiently uniformly dispersed in the electrode mixture layer, the conductive aid sufficiently fills the voids between the active materials, and the diffusion of Li ions is inhibited. There are few pores passing through. Therefore, the electrode according to the first embodiment can realize a nonaqueous electrolyte battery that can exhibit excellent output performance.
  • a non-aqueous electrolyte battery comprises an electrode according to the first embodiment as a positive electrode, a negative electrode, and a non-aqueous electrolyte.
  • the nonaqueous electrolyte battery according to the second embodiment includes the electrode according to the first embodiment as a positive electrode.
  • the positive electrode can include the electrode mixture layer described in the first embodiment as a positive electrode mixture layer.
  • the positive electrode mixture layer can include the active material described in the first embodiment as a positive electrode active material.
  • the positive electrode can further comprise a positive electrode current collector.
  • the positive electrode current collector can use the current collector described in the first embodiment.
  • the nonaqueous electrolyte battery according to the second embodiment further includes a negative electrode.
  • the negative electrode can include a negative electrode current collector and a negative electrode mixture layer provided on the negative electrode current collector.
  • the negative electrode mixture layer may be provided on either side of the negative electrode current collector or may be provided on both sides thereof.
  • the negative electrode mixture layer can include a negative electrode active material, a conductive additive, and a binder.
  • the negative electrode current collector can also include a portion not carrying the negative electrode mixture layer on the surface. This portion can also, for example, act as a negative current collector tab. Alternatively, the negative electrode can also include a negative electrode current collection tab separate from the negative electrode current collector.
  • the negative electrode is prepared by suspending a negative electrode active material, a binder and a conductive auxiliary agent in an appropriate solvent to prepare a paint for producing a negative electrode, applying this paint on the surface of a negative electrode current collector, and drying it After forming a layer, it can produce by giving a press.
  • the positive electrode and the negative electrode can be arranged such that the positive electrode mixture layer and the negative electrode mixture layer face each other to constitute an electrode group. Between the positive electrode mixture layer and the negative electrode mixture layer, a member which transmits lithium ions but does not transmit electricity, for example, a separator can be disposed.
  • the electrode group can have various structures.
  • the electrode group may have a stacked structure or may have a wound structure.
  • the stack structure has, for example, a structure in which a plurality of negative electrodes and a plurality of positive electrodes are stacked with a separator interposed between the negative electrode and the positive electrode.
  • the wound-type electrode group may be, for example, a can-type structure in which a negative electrode and a positive electrode are stacked with a separator interposed therebetween and wound, or by pressing the can-type structure It may be a flat structure obtained.
  • the electrode group can also have a structure other than the stacked type and the wound type.
  • the positive current collection tab can be electrically connected to the positive electrode terminal.
  • the negative electrode current collection tab can be electrically connected to the negative electrode terminal.
  • the positive electrode terminal and the negative electrode terminal can extend from the electrode group.
  • the electrode group can be housed in the exterior member.
  • the exterior member may have a structure capable of extending the positive electrode terminal and the negative electrode terminal to the outside.
  • the package member may be configured to include two external terminals, each of which is electrically connected to each of the positive electrode terminal and the negative electrode terminal.
  • the exterior member itself can function as either the positive electrode terminal or the positive electrode terminal.
  • the nonaqueous electrolyte battery according to the second embodiment further comprises a nonaqueous electrolyte.
  • the non-aqueous electrolyte can be impregnated into the electrode group.
  • the non-aqueous electrolyte can be accommodated in the exterior member.
  • the positive electrode and the positive electrode for example, those described in the first embodiment can be used.
  • the proportions of the positive electrode active material, the conductive additive and the binder in the positive electrode mixture layer are 70% by weight or more and 95% by weight or less, 1% by weight or more and 20% by weight or less, and 1% by weight or more and 10% by weight or less Is preferred. More preferable blending ratios are 80 wt% or more and 95 wt% or less, 3 wt% or more and 10 wt% or less, and 2 wt% or more and 10 wt% or less.
  • negative electrode current collector for example, those described in the first embodiment can be used.
  • the negative electrode active material for example, those described in the first embodiment can be used.
  • a graphitic material and a carbonaceous material can also be used as the negative electrode active material.
  • the graphitic material and the carbonaceous material include natural graphite, artificial graphite, coke, vapor grown carbon fiber, mesophase pitch carbon fiber, spherical carbon, and resin-fired carbon.
  • the negative electrode active material a mixture of those described in the first embodiment and the graphitic material and / or the carbonaceous material can also be used.
  • a carbon material can be used as a conductive support agent which can be contained in the negative electrode mixture layer.
  • a carbon material carbon black, coke, carbon fiber, graphite etc. can be mentioned, for example.
  • the binder is used to bond the negative electrode active material and the negative electrode current collector.
  • a binder which a negative electrode mixture layer can contain the thing similar to what can be used by the positive electrode mixture layer can be used.
  • the negative electrode active material, the conductive auxiliary agent, and the binder contained in the negative electrode mixture layer are compounded in a proportion of 70% by weight to 96% by weight, 2% by weight to 20% by weight, and 2% by weight to 10% by weight, respectively. Is preferred.
  • the amount of the conductive additive By setting the amount of the conductive additive to 2% by weight or more, the current collection performance of the negative electrode mixture layer can be improved. Further, by setting the amount of the binder to 2% by weight or more, the binding property between the negative electrode mixture layer and the negative electrode current collector can be enhanced, and excellent cycle characteristics can be expected.
  • the separator is made of an insulating material, and can prevent electrical contact between the positive electrode and the negative electrode.
  • the separator is made of a material through which the non-aqueous electrolyte can pass, or has a shape through which the non-aqueous electrolyte can pass.
  • the separator of the porous film and nonwoven fabric which consist of 1 type or 2 types selected from the group which consists of polyethylene, a polypropylene, a polyethylene terephthalate, a cellulose, and vinylon can be mentioned.
  • the nonaqueous electrolyte can include, for example, a nonaqueous solvent, and an electrolyte and an additive dissolved in the nonaqueous solvent.
  • the non-aqueous solvent may be a known non-aqueous solvent used in non-aqueous electrolyte batteries.
  • a first example of non-aqueous solvent is cyclic carbonate such as ethylene carbonate (EC) and propylene carbonate (PC).
  • Second examples of non-aqueous solvents are linear carbonates such as dimethyl carbonate, ethyl methyl carbonate and diethyl carbonate; ⁇ -butyrolactone, acetonitrile, methyl propionate, ethyl propionate; cyclic ethers such as tetrahydrofuran and 2-methyltetrahydrofuran; It is a chain ether such as dimethoxyethane and diethoxyethane.
  • the solvent of the second example is generally of low viscosity compared to the solvent of the first example.
  • the non-aqueous solvent may be a solvent obtained by mixing the solvent of the first example described above and the solvent of the second example.
  • the electrolyte is, for example, an alkali salt, preferably a lithium salt.
  • the electrolyte comprises at least one lithium salt.
  • lithium salts are lithium hexafluorophosphate (LiPF 6 ), lithium hexafluoroarsenate (LiAsF 6 ), lithium tetrafluoroborate (LiBF 4 ) and lithium trifluoromethanesulfonate (LiCF 3 SO 3 ) It is.
  • the electrolyte is lithium hexafluorophosphate (LiPF 6 ).
  • the concentration of the electrolyte in the non-aqueous electrolyte is preferably 0.5 to 2 mol / L.
  • the negative electrode current collection tab, the positive electrode current collection tab, the negative electrode terminal and the positive electrode terminal are preferably made of a material having high electrical conductivity. When connected to the current collector, in order to reduce the contact resistance, these members are preferably made of the same material as the current collector.
  • a metal container or a laminate film container can be used, but it is not particularly limited.
  • a non-aqueous electrolyte battery excellent in impact resistance and long-term reliability can be realized.
  • a laminate film container as the exterior material it is possible to realize a non-aqueous electrolyte battery excellent in corrosion resistance, and to reduce the weight of the non-aqueous electrolyte battery.
  • the metal container for example, one having a wall thickness in the range of 0.2 to 5 mm can be used.
  • the metal container more preferably has a wall thickness of 0.5 mm or less.
  • the metal container preferably contains at least one selected from the group consisting of Fe, Ni, Cu, Sn and Al.
  • the metal container can be made of, for example, aluminum or an aluminum alloy.
  • the aluminum alloy is preferably an alloy containing an element such as magnesium, zinc or silicon.
  • the alloy contains a transition metal such as iron, copper, nickel, or chromium, the content is preferably 1% by weight or less.
  • the laminated film container can be produced, for example, using a laminated film having a thickness in the range of 0.1 to 2 mm.
  • the thickness of the laminate film is more preferably 0.2 mm or less.
  • a multilayer film including a metal layer and a resin layer sandwiching the metal layer is used.
  • the metal layer preferably contains a metal containing at least one selected from the group consisting of Fe, Ni, Cu, Sn and Al.
  • the metal layer is preferably aluminum foil or aluminum alloy foil in order to reduce the weight.
  • polymeric materials such as polypropylene (PP), polyethylene (PE), nylon, polyethylene terephthalate (PET) can be used.
  • the laminated film can be molded into the shape of the exterior material by sealing by heat fusion.
  • the shape of the exterior material may, for example, be flat (thin), square, cylindrical, coin or button.
  • the sheathing material can have various dimensions depending on the application.
  • the exterior material can be made smaller according to the size of the electronic devices to be mounted.
  • the container may be a container for a large battery.
  • FIG. 6 is a schematic cutaway perspective view of a first example nonaqueous electrolyte battery according to a second embodiment.
  • 7 is a schematic enlarged cross-sectional view of a portion A of FIG.
  • the nonaqueous electrolyte battery 100 shown in FIGS. 6 and 7 includes a flat electrode group 1.
  • the flat electrode group 1 includes a negative electrode 2, a positive electrode 3, and a separator 4.
  • the negative electrode 2 includes a negative electrode current collector 2a and a negative electrode mixture layer 2b supported on the negative electrode current collector 2a.
  • the positive electrode 3 includes a positive electrode current collector 3a and a positive electrode mixture layer 3b supported on the positive electrode current collector 3a. That is, the positive electrode 3 has the same structure as the electrode 10 of one example according to the first embodiment shown in FIG.
  • the negative electrode 2 and the positive electrode 3 are stacked in a state in which the separator 4 is interposed between the negative electrode mixture layer 2b and the positive electrode mixture layer 3b.
  • Such an electrode group 1 can be obtained by the following procedure. First, one flat plate-like negative electrode 2 and one flat plate-like positive electrode 3 are laminated with the separator 4 interposed therebetween. Next, another separator 4 is laminated on the positive electrode mixture layer 3b not facing the negative electrode 2 to form a laminate. The laminate is wound with the negative electrode 2 on the outside. Next, after removing the winding core, it is pressed to form a flat shape. Thus, the electrode group 1 shown in FIGS. 6 and 7 can be obtained.
  • a band-like negative electrode terminal 5 is electrically connected to the negative electrode 2.
  • a strip-shaped positive electrode terminal 6 is electrically connected to the positive electrode 3.
  • the nonaqueous electrolyte battery 100 shown in FIGS. 6 and 7 further includes an outer packaging bag 7 made of a laminated film as a container.
  • the electrode group 1 is accommodated in an outer packaging bag 7 made of a laminate film in a state where the end portions of the negative electrode terminal 5 and the positive electrode terminal 6 are extended from the outer packaging bag 7.
  • a non-aqueous electrolyte (not shown) is accommodated in the laminate film outer packaging bag 7.
  • the non-aqueous electrolyte is impregnated in the electrode group 1.
  • the outer bag 7 is heat-sealed at its peripheral edge, thereby sealing the electrode assembly 1 and the non-aqueous electrolyte.
  • FIG. 8 is a partially cutaway perspective view of a non-aqueous electrolyte battery of a second example according to the second embodiment.
  • the non-aqueous electrolyte battery 100 shown in FIG. 8 is largely different from the non-aqueous electrolyte battery 100 of the first example in that the packaging material is composed of a metal container 7a and a sealing plate 7b.
  • a non-aqueous electrolyte battery 100 shown in FIG. 8 includes an electrode group 1 similar to the electrode group 1 of the non-aqueous electrolyte battery 100 of the first example.
  • the difference from the first example is that, in the second example shown in FIG. 8, the member 5 a used as the negative electrode terminal 5 in the first example is used as a negative electrode tab, and in the first example, the positive electrode The point is that the member 6a used as the terminal 6 is used as the positive electrode tab.
  • such an electrode group 1 is accommodated in a metal container 7a.
  • the metal container 7a further accommodates the non-aqueous electrolyte.
  • the metal container 7a is sealed by a metal sealing plate 7b.
  • the sealing plate 7 b is provided with a negative electrode terminal 5 and a positive electrode terminal 6.
  • An insulating member 7c is disposed between the positive electrode terminal 6 and the sealing plate 7b. Thereby, the positive electrode terminal 6 and the sealing plate 7b are electrically insulated.
  • the negative electrode terminal 5 is connected to the negative electrode tab 5a as shown in FIG.
  • the positive electrode terminal 6 is connected to the positive electrode tab 6a.
  • nonaqueous electrolyte battery according to the second embodiment includes the electrode according to the first embodiment, it can exhibit excellent output performance.
  • Example 1-1 the non-aqueous electrolyte battery of Example 1-1 was manufactured according to the following procedure.
  • particles of graphite A as particles of a first carbon material and particles of acetylene black A as particles of a second carbon material were prepared.
  • the aspect ratio was 1.9
  • the intensity ratio G 1 / D 1 was 5
  • the average particle size was 4.2.
  • the aspect ratio was 1.1
  • the intensity ratio G 2 / D 2 was 1.38
  • the average particle size was 0.52.
  • Example 1-1 particles of graphite A and particles of acetylene black A were weighed so as to have a weight ratio of 2: 3. Then, they were stirred at a rotation speed of 500 rpm in a Henschel mixer for 1 hour. That is, in Example 1-1, the conductive aid for the positive electrode was subjected to pre-dispersion.
  • the mixed powder obtained by pre-dispersion was dissolved in N-methylpyrrolidone and stirred at 2000 rpm for 2 minutes using “Neriterou” manufactured by Shinky Co., Ltd. Then, polyvinylidene fluoride as a binder was uniformly added in three portions to the obtained dispersion, and each time the addition was carried out, the mixture was stirred for 2 minutes at a rotation speed of 2000 rpm by Nerichiro. The addition of the binder here was adjusted so that the weight ratio of the conductive additive to the binder was 1: 1 in the finally obtained dispersion.
  • particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 1/3 Co 1/3 Mn 1/3 O 2 were added to the obtained dispersion as a positive electrode active material.
  • the particles had an average primary particle size of 0.5 ⁇ m, and secondary particles formed by aggregating them had an average secondary diameter of 7 ⁇ m.
  • the weight ratio of a positive electrode active material, a conductive support agent, and a binder might be set to 90: 5: 5.
  • N-methylpyrrolidone was added to the dispersion to adjust the solid content of the dispersion to 70%.
  • Example 1-1 solid kneading was performed when preparing a paint for a positive electrode.
  • the dispersion obtained by solid kneading was diluted with N-methylpyrrolidone in two portions to make the solid content of the dispersion 60%.
  • the dispersion thus obtained was stirred at 2000 rpm for 5 minutes in Nerichiro.
  • This paste-like positive electrode paint was uniformly applied on both the front and back sides of a positive electrode current collector made of an aluminum foil having a strip thickness of 20 ⁇ m, and the coated film was dried.
  • the coating amount of the positive electrode paint was 150 g / m 2 .
  • coated remained on the front and back at the positive electrode collector.
  • the paint film after drying of the paint and the positive electrode current collector were pressed, and these were cut into predetermined dimensions. Subsequently, the positive electrode tab was welded to the positive electrode paint uncoated portion.
  • a positive electrode comprising the positive electrode current collector and the positive electrode mixture layer formed on both sides of the positive electrode current collector was obtained.
  • the density of the positive electrode mixture layer obtained by pressing was 3.3 g / m 2 .
  • Li 4 Ti 5 O 12 lithium titanate (LTO) having a composition represented by Li 4 Ti 5 O 12 as a negative electrode active material was prepared.
  • graphite and acetylene black were prepared. These were mixed at a weight ratio of 1: 4 to obtain a conductive aid.
  • Polyvinylidene fluoride was prepared as a binder. These materials were mixed so that the weight ratio of active material: conductive auxiliary agent: binder was 90: 5: 5. The mixture thus obtained was dissolved in N-methylpyrrolidone as a solvent and mixed. Thus, a paste-like negative electrode paint was prepared.
  • the paste-like negative electrode paint was uniformly applied on both the front and back sides of a negative electrode current collector made of aluminum foil having a strip thickness of 20 ⁇ m, and the coated film was dried.
  • the coating amount of the negative electrode paint was 150 g / m 2 .
  • the negative electrode current collector was left with an area where no paint was applied on either side.
  • the paint film after drying of the paint and the negative electrode current collector were pressed and cut into predetermined dimensions. Then, the negative electrode tab was welded to the negative electrode paint uncoated portion.
  • a negative electrode including the negative electrode current collector and the negative electrode mixture layer formed on both sides of the negative electrode current collector was obtained.
  • Nonaqueous Electrolyte A mixed solvent of ethylene carbonate (EC) and ethylmethyl carbonate (EMC) was prepared as a nonaqueous solvent. In this mixed solvent, the weight ratio of EC: EMC was 1: 2. In this mixed solvent, lithium hexafluorophosphate LiPF 6 was dissolved at a concentration of 1.0 M as an electrolyte. Thus, a non-aqueous electrolyte was prepared.
  • EC ethylene carbonate
  • EMC ethylmethyl carbonate
  • a container made of a laminate film having a width of 80 mm, a height of 110 mm and a thickness of 3 mm, and an opening, and a positive electrode terminal and a negative electrode terminal are provided.
  • a sealing plate was prepared. The sealing plate further had a liquid inlet and a safety valve.
  • the positive electrode tab of the previously produced electrode group was connected to the positive electrode terminal of the sealing plate.
  • the negative electrode tab of the previously prepared electrode group was connected to the negative electrode terminal of the sealing plate.
  • the electrode group was housed in the prepared container.
  • the opening of the container was sealed with a sealing plate.
  • the previously prepared non-aqueous electrolyte was injected into the container through the injection port of the sealing plate to impregnate the electrode group.
  • the square nonaqueous electrolyte battery of Example 1-1 was produced.
  • Example 1-2 the nonaqueous electrolyte of Example 1-2 was prepared by the same procedure as in Example 1-1 except that particles of graphite B were used as the first carbon material in preparing the positive electrode paint. A battery was made.
  • the aspect ratio was 1.78
  • the intensity ratio G 1 / D 1 was 5.8, and the average particle size was 7.0.
  • Examples 1-3 to 1-7 the same procedures as in Example 1-1 except that particles of the carbon material shown in Table 1 below were used as the second carbon material in the preparation of the positive electrode paint Thus, each of the non-aqueous electrolyte batteries of Examples 1-3 to 1-7 was manufactured.
  • the aspect ratio was 1.12
  • the intensity ratio G 2 / D 2 was 1.45
  • the average particle size was 2.1.
  • the aspect ratio was 1.05
  • the intensity ratio G 2 / D 2 was 1.59
  • the average particle size was 0.53.
  • the aspect ratio was 1.08, the intensity ratio G 2 / D 2 was 1.24, and the average particle size was 0.53.
  • the aspect ratio was 1.07, the intensity ratio G 2 / D 2 was 1.19, and the average particle size was 0.51.
  • the aspect ratio was 1.12, the intensity ratio G 2 / D 2 was 1.23, and the average particle size was 0.52.
  • Example 1-8 In Example 1-8, except that pre-dispersion was performed using a weight ratio of particles of graphite A and particles of acetylene black A at a weight ratio of 2: 2.1 when preparing a positive electrode paint.
  • the non-aqueous electrolyte battery of Example 1-8 was produced in the same manner as in No. 1.
  • Example 1-9 is the same as Example 1-1 except that in the preparation of the positive electrode paint, pre-dispersion is performed using particles of graphite A and particles of acetylene black A in a weight ratio of 2: 5.
  • the nonaqueous electrolyte battery of Example 1-9 was fabricated by the same procedure.
  • Examples 1-10 to 1-13 are the same as Example 1-1 except that the positive electrode active material was changed to one having the composition described in Table 3 below, and the coated amount of the positive electrode was changed.
  • the nonaqueous electrolyte batteries of Examples 1-10 to 1-13 were manufactured according to the procedure.
  • Example 1-10 particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 5/10 Co 2/10 Mn 3/10 O 2 were used as a positive electrode active material.
  • the coating amount of the positive electrode was 140 g / m 2 .
  • the average primary particle size and the average secondary particle size of the positive electrode active material particles used were the same as those of the positive electrode active material particles used in Example 1-1.
  • Example 1-11 particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 6/10 Co 2/10 Mn 2/10 O 2 were used as a positive electrode active material.
  • the coating amount of the positive electrode was set to 130 g / m 2 .
  • the average primary particle size and the average secondary particle size of the positive electrode active material particles used were the same as those of the positive electrode active material particles used in Example 1-1.
  • Example 1-12 particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 5/10 Co 3.5 / 10 Mn 1.5 / 10 O 2 were used as a positive electrode active material.
  • the coating amount of the positive electrode was 140 g / m 2 .
  • the average primary particle size and the average secondary particle size of the positive electrode active material particles used were the same as those of the positive electrode active material particles used in Example 1-1.
  • Example 1-13 particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 4.5 / 10 Co 3.5 / 10 Mn 2/10 O 2 were used as a positive electrode active material. Moreover, the coating amount of the positive electrode was 145 g / m 2 . The average primary particle size and the average secondary particle size of the positive electrode active material particles used were the same as those of the positive electrode active material particles used in Example 1-1.
  • Example 2-1 In Example 2-1, the particles of spinel-type lithium manganese oxide LiMn 2 O 4 were used as the positive electrode active material, and the coated amount of the positive electrode paint was changed to 255 g / m 2 , except for using Example 1-1 and The non-aqueous electrolyte battery of Example 2-1 was fabricated by the same procedure.
  • the positive electrode active material particles used had an average primary particle size of 1 ⁇ m and an average secondary particle size of 9 ⁇ m.
  • Example 3-1 is the same as example 1-1 except that particles of olivine-type lithium iron phosphate LiFePO 4 are used as the positive electrode active material, and that the coating amount of the positive electrode paint is 165 g / m 2.
  • the nonaqueous electrolyte battery of Example 3-1 was produced according to the procedure of The positive electrode active material particles used had an average primary particle size of 0.05 ⁇ m and an average secondary particle size of 1 ⁇ m.
  • Example 4-1 In Example 4-1, the procedure of Example 1-1 is followed except that particles of lithium cobaltate LiCoO 2 are used as the positive electrode active material, and that the coating amount of the positive electrode paint is 165 g / m 2. A non-aqueous electrolyte battery of Example 4-1 was produced. The positive electrode active material particles used did not form secondary particles, and the average primary particle diameter was 8 ⁇ m.
  • Examples 5-1, 6-1, 7-1 and 8-1 In Examples 5-1, 6-1, 7-1, and 8-1, the procedure is the same as that of Example 1-1 except that the negative electrode active material is changed and the coating amount of the negative electrode paint is changed. Each non-aqueous electrolyte battery was produced. That is, in these examples, a non-aqueous electrolyte battery was produced using the same positive electrode as that of Example 1-1.
  • Example 5-1 MCF (mesophase pitch carbon fiber) was used as the negative electrode active material, and the coating amount of the negative electrode paint was 75 g / m 2 .
  • Example 6-1 titanium oxide TiO 2 (B) having a monoclinic crystal structure was used as the negative electrode active material, and the coating amount of the negative electrode paint was 120 g / m 2 .
  • Example 7-1 the coating amount of the negative electrode paint was 100 g / m 2 using niobium titanium complex oxide Nb 2 TiO 7 (NTO) having a monoclinic crystal structure as the negative electrode active material.
  • NTO niobium titanium complex oxide Nb 2 TiO 7
  • Example 8-1 a lithium niobium titanium composite oxide Li 2 NaTi 5 NbO 14 (LNT) having an orthorhombic crystal structure is used as the negative electrode active material, and the coating amount of the negative electrode coating is 210 g / m 2 . did.
  • Example 9-1 the non-aqueous electrolyte battery of Example 9-1 was prepared by the same procedure as Example 1-1 except that particles of graphene were used as the first carbon material in preparing the positive electrode paint. Was produced.
  • the aspect ratio was 1.95
  • the intensity ratio G 1 / D 1 was 6.2
  • the average particle size was 5.3 ⁇ m.
  • Comparative Example 1-1 a non-aqueous electrolyte battery of Comparative Example 1-1 was produced in the same manner as in Example 1-1 except that the positive electrode was produced in the following procedure.
  • the mixed powder obtained by pre-dispersion was dissolved in N-methylpyrrolidone and stirred at 2000 rpm for 10 minutes using “Neriterou” manufactured by Shinky Co., Ltd. Subsequently, polyvinylidene fluoride was added as a binder to the obtained dispersion, and the weight ratio of the conductive additive to the binder was adjusted to 1: 1.
  • the dispersion thus obtained was stirred in Nertaro at a rotation speed of 2000 rpm for 10 minutes.
  • a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 1/3 Co 1/3 Mn 1/3 O 2 was added to the obtained dispersion as a positive electrode active material.
  • the weight ratio of an active material, a conductive support agent, and a binder might be set to 90: 5: 5.
  • N-methyl pyrrolidone was added to the dispersion to adjust the solid content of the dispersion to 60%.
  • the dispersion thus obtained was then stirred at 2000 rpm for 40 minutes in Nerichiro. Thus, a paste-like positive electrode paint was obtained.
  • Comparative Example 1-1 a positive electrode was produced in the same manner as in Example 1-1 except that this paste-like positive electrode paint was used.
  • Comparative Example 1-2 the non-aqueous electrolyte battery of Comparative Example 1-2 was produced in the same manner as in Example 1-1 except that the positive electrode was produced in the following procedure.
  • particles of graphite A, particles of acetylene black B, and polyvinylidene fluoride as a binder were weighed so as to have a weight ratio of 2: 3: 5. Then, they were dissolved in N-methylpyrrolidone and stirred at 2000 rpm for 20 minutes using “Neritaro” manufactured by Shinky Co., Ltd.
  • a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 1/3 Co 1/3 Mn 1/3 O 2 was added to the obtained dispersion as a positive electrode active material.
  • the weight ratio of a positive electrode active material, a conductive support agent, and a binder might be set to 90: 5: 5.
  • N-methyl pyrrolidone was added to the dispersion to adjust the solid content of the dispersion to 70%, and the dispersion thus obtained was subjected to four further stirrings. For each stirring, the dispersion was stirred at 2000 rpm for 10 minutes in Nerichiro. After each round of stirring, the dispersion was cooled for 10 minutes at room temperature. That is, in Comparative Example 1-2, solid kneading was performed when preparing the paint for the positive electrode.
  • the dispersion obtained by solid kneading was diluted with N-methylpyrrolidone to make the solid content of the dispersion 60%.
  • the dispersion thus obtained was stirred at 2000 rpm for 20 minutes in Nerichiro. Thus, a paste-like positive electrode paint was obtained.
  • Comparative Example 1-2 a positive electrode was produced in the same manner as in Example 1-1 except that this paste-like positive electrode paint was used.
  • Comparative Example 1-3 the non-aqueous electrolyte battery of Comparative Example 1-3 was produced in the same manner as in Example 1-1 except that the positive electrode was produced in the following procedure.
  • the mixed powder obtained by pre-dispersion was dissolved in N-methylpyrrolidone and stirred at 2000 rpm for 10 minutes using “Neriterou” manufactured by Shinky Co., Ltd.
  • polyvinylidene fluoride was added to the obtained dispersion as a binder. Under the present circumstances, it adjusted so that the weight ratio of a conductive support agent and a binder might be set to 1: 1.
  • the obtained dispersion was stirred at a rotation speed of 2000 rpm for 10 minutes in Nerichiro. Thus, by mixing NMP and the binder in this order, it is possible to prevent aggregation of the conductive aid.
  • a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 1/3 Co 1/3 Mn 1/3 O 2 was added to the obtained dispersion as a positive electrode active material.
  • the weight ratio of an active material, a conductive support agent, and a binder might be set to 90: 5: 5.
  • N-methylpyrrolidone was added to the dispersion to adjust the solid content of the dispersion to 70%.
  • the dispersion thus obtained was then subjected to 10 additional stirrings. In each stirring, stirring was performed at 2000 rpm for 10 minutes in Nerichiro. After each round of stirring, the dispersion was cooled for 10 minutes at room temperature.
  • the resulting dispersion was then diluted with N-methyl pyrrolidone to bring the solids content of the dispersion to 60%.
  • the dispersion thus obtained was stirred at 2000 rpm for 20 minutes in Nerichiro. Thus, a paste-like positive electrode paint was obtained.
  • Comparative Example 1-3 a positive electrode was produced in the same manner as in Example 1-1 except that this paste-like positive electrode paint was used.
  • Comparative Example 1-4 the nonaqueous electrolyte of Comparative Example 1-4 was prepared according to the same procedure as Example 1-1 except that particles of graphite C were used as the first carbon material in preparing the positive electrode paint. A battery was made.
  • the aspect ratio was 2.71
  • the intensity ratio G 1 / D 1 was 5.4
  • the average particle size was 5.5 ⁇ m.
  • Comparative Example 1-5 the nonaqueous electrolyte of Comparative Example 1-5 was prepared by the same procedure as Example 1-1 except that particles of graphite D were used as the first carbon material in preparing the positive electrode paint. A battery was made.
  • the aspect ratio was 1.34
  • the intensity ratio G 1 / D 1 was 5.2
  • the average particle size was 4.9 ⁇ m.
  • Comparative Examples 1-6 to 1-9 are the same as Example 1-1 except that in the pre-dispersion, the weight ratio of the particles of graphite A to acetylene black A was changed as shown in Table 2 below. Each non-aqueous electrolyte battery of Comparative Examples 1-6 to 1-9 was fabricated by the procedure.
  • Comparative Examples 1-10 to 1-13 use Examples 1-10 to 1-13, respectively, except that particles of graphite C similar to those used in Comparative Example 1-4 are used as the first carbon material.
  • Each non-aqueous electrolyte battery of Comparative Examples 1-10 to 1-13 was fabricated in the same manner.
  • Comparative Example 1-14 In Comparative Example 1-14, the non-aqueous electrolyte battery of Comparative Example 1-14 was produced in the same manner as in Example 1-1 except that the positive electrode was produced according to the following procedure.
  • particles of graphite A as particles of a first carbon material and particles of acetylene black A as particles of a second carbon material were prepared.
  • the aspect ratio was 1.9
  • the intensity ratio G 1 / D 1 was 5, and the average particle size was 4.2.
  • the aspect ratio was 1.1
  • the intensity ratio G 2 / D 2 was 1.38
  • the average particle size was 0.52. That is, the same particles of graphite A and particles of acetylene black A as used in Example 1-1 were used.
  • the mixed powder obtained by pre-dispersion was dissolved in N-methylpyrrolidone and stirred at 2000 rpm for 2 minutes using “Neriterou” manufactured by Shinky Co., Ltd. Then, polyvinylidene fluoride as a binder was uniformly added in three portions to the obtained dispersion, and each time the addition was carried out, the mixture was stirred for 2 minutes at a rotation speed of 2000 rpm by Nerichiro. The addition of the binder here was adjusted so that the weight ratio of the conductive additive to the binder was 1: 1 in the finally obtained dispersion.
  • particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 1/3 Co 1/3 Mn 1/3 O 2 were added to the obtained dispersion as a positive electrode active material.
  • the particles had an average primary particle size of 0.5 ⁇ m, and secondary particles formed by aggregating them had an average secondary diameter of 7 ⁇ m.
  • the weight ratio of a positive electrode active material, a conductive support agent, and a binder might be set to 90: 5: 5.
  • N-methylpyrrolidone was added to the dispersion to adjust the solid content of the dispersion to 70%.
  • the dispersion thus obtained was then subjected to four further stirrings. For each stirring, the dispersion was stirred at 2000 rpm for 2 minutes in Nerichiro. After each round of stirring, the dispersion was cooled for 10 minutes at room temperature. That is, in Comparative Example 1-14, solid kneading was performed when preparing the paint for the positive electrode.
  • the dispersion obtained by solid kneading was diluted with N-methylpyrrolidone to make the solid content of the dispersion 60%.
  • the dispersion thus obtained was stirred at 2000 rpm for 5 minutes in Nerichiro.
  • Comparative Example 1-14 a positive electrode was produced in the same manner as in Example 1-1 except that this paste-like positive electrode paint was used.
  • Comparative Example 1-15 In Comparative Example 1-15, the non-aqueous electrolyte battery of Comparative Example 1-15 was produced in the same manner as in Example 1-1 except that the positive electrode was produced in the following procedure.
  • particles of graphite A as particles of a first carbon material and particles of acetylene black A as particles of a second carbon material were prepared.
  • the aspect ratio was 1.9
  • the intensity ratio G 1 / D 1 was 5, and the average particle size was 4.2.
  • the aspect ratio was 1.1
  • the intensity ratio G 2 / D 2 was 1.38
  • the average particle size was 0.52. That is, the same particles of graphite A and particles of acetylene black A as used in Example 1-1 were used.
  • the mixed powder obtained by pre-dispersion was dissolved in N-methylpyrrolidone and stirred at 2000 rpm for 2 minutes using “Neriterou” manufactured by Shinky Co., Ltd. Then, polyvinylidene fluoride as a binder was uniformly added in three portions to the obtained dispersion, and each time the addition was carried out, the mixture was stirred for 2 minutes at a rotation speed of 2000 rpm by Nerichiro. The addition of the binder here was adjusted so that the weight ratio of the conductive additive to the binder was 1: 1 in the finally obtained dispersion.
  • particles of a lithium-containing nickel-cobalt-manganese composite oxide having a composition represented by LiNi 1/3 Co 1/3 Mn 1/3 O 2 were added to the obtained dispersion as a positive electrode active material.
  • the particles had an average primary particle size of 0.5 ⁇ m, and secondary particles formed by aggregating them had an average secondary diameter of 7 ⁇ m.
  • the weight ratio of a positive electrode active material, a conductive support agent, and a binder might be set to 90: 5: 5.
  • N-methylpyrrolidone was added to the dispersion to adjust the solid content of the dispersion to 70%.
  • the dispersion thus obtained was then subjected to four further stirrings. For each stirring, the dispersion was stirred at 2000 rpm for 2 minutes in Nerichiro. After each round of stirring, the dispersion was cooled for 10 minutes at room temperature. That is, in Comparative Example 1-15, solid kneading was performed when preparing the paint for the positive electrode.
  • the dispersion obtained by solid kneading was diluted with N-methylpyrrolidone to make the solid content of the dispersion 60%.
  • the dispersion thus obtained was stirred at 2000 rpm for 5 minutes in Nerichiro.
  • Comparative Example 1-15 a positive electrode was produced in the same manner as in Example 1-1 except that this paste-like positive electrode paint was used.
  • Comparative Examples 2-1 to 4-1 In Comparative Examples 2-1 to 4-1, the particles of Graphite C similar to those used in Comparative Example 1-4 were used as the first carbon material, and Example 2-1 to 4-1, respectively. Each non-aqueous electrolyte battery of Comparative Examples 2-1 to 4-1 was manufactured in the same manner.
  • Comparative Examples 5-1 to 8-1 In Comparative Examples 5-1 to 8-1, Comparative Example 5 is carried out in the same manner as in Examples 5-1 to 8-1, respectively, except that the positive electrode produced in the same manner as Comparative example 1-4 is used. Each non-aqueous electrolyte battery of 1-8-1 was produced.
  • each non-aqueous electrolyte battery was initially charged at a temperature of 25 ° C. and at a rate of 0.1 C until the battery voltage reached 2.7 V. Each non-aqueous electrolyte cell was then discharged at a rate of 1 C until the cell voltage reached 1.5V. The capacity discharged at this time was taken as a test capacity.
  • each non-aqueous electrolyte battery was initially charged at a temperature of 25 ° C. and at a rate of 0.1 C until the battery voltage reached 2.8 V. Each non-aqueous electrolyte cell was then discharged at a rate of 1 C until the cell voltage reached 1.5V. The capacity discharged at this time was taken as a test capacity.
  • Example 5-1 and Comparative Example 5-1 First, each non-aqueous electrolyte battery was initially charged at a temperature of 25 ° C. and at a rate of 0.1 C until the battery voltage reached 4.2 V. Each non-aqueous electrolyte cell was then discharged at a rate of 1 C until the cell voltage reached 3.0V. The capacity discharged at this time was taken as a test capacity.
  • each non-aqueous electrolyte battery was initially charged at a temperature of 25 ° C. and at a rate of 0.1 C until the battery voltage reached 2.9 V. Each non-aqueous electrolyte cell was then discharged at a rate of 1 C until the cell voltage reached 1.5V. The capacity discharged at this time was taken as a test capacity.
  • Examples 1-1 to 1-13, 4-1 and 9-1 and comparative examples 1-1 to 1-15 and 4-1 Each non-aqueous electrolyte battery in the shipping state was constant current charged at a temperature of 25 ° C. and at a rate of 1 C until the battery voltage reached 2.7 V. Next, each non-aqueous electrolyte battery was charged at a constant voltage to a current value of 0.05C. Each non-aqueous electrolyte cell was then discharged at a temperature of 25 ° C. and at a rate of 10 C until the cell voltage reached 1.5V. The value obtained by dividing the capacity obtained at this time by the inspection capacity was taken as the discharge capacity retention rate.
  • Examples 2-1 and 3-1 and Comparative Examples 2-1 and 3-1 Each shipping non-aqueous electrolyte battery was constant current charged at a temperature of 25 ° C. and at a rate of 1 C until the battery voltage reached 2.8 V. Next, each non-aqueous electrolyte battery was charged at a constant voltage to a current value of 0.05C. Each non-aqueous electrolyte cell was then discharged at a temperature of 25 ° C. and at a rate of 10 C until the cell voltage reached 1.5V. The value obtained by dividing the capacity obtained at this time by the inspection capacity was taken as the discharge capacity retention rate.
  • Example 5-1 and Comparative Example 5-1 Each shipping non-aqueous electrolyte battery was constant current charged at a temperature of 25 ° C. and at a rate of 1 C until the battery voltage reached 4.2 V. Next, each non-aqueous electrolyte battery was charged at a constant voltage to a current value of 0.05C. Each non-aqueous electrolyte cell was then discharged at a temperature of 25 ° C. and at a rate of 10 C until the cell voltage reached 3.0 V. The value obtained by dividing the capacity obtained at this time by the inspection capacity was taken as the discharge capacity retention rate.
  • Example 6-1, 7-1 and 8-1 and comparative examples 6-1, 7-1 and 8-1 Each non-aqueous electrolyte battery in the shipping condition was constant current charged at a temperature of 25 ° C. and at a rate of 1 C until the battery voltage reached 2.9 V. Next, each non-aqueous electrolyte battery was charged at a constant voltage to a current value of 0.05C. Each non-aqueous electrolyte cell was then discharged at a temperature of 25 ° C. and at a rate of 10 C until the cell voltage reached 1.5V. The value obtained by dividing the capacity obtained at this time by the inspection capacity was taken as the discharge capacity retention rate.
  • the conductive support agent contained in the positive electrode mixture layer of the positive electrode of each non-aqueous electrolyte battery was subjected to the measurement of the aspect ratio and the average particle diameter by the procedure described above. Further, the positive electrode mixture layer of the positive electrode of each non-aqueous electrolyte battery was subjected to the measurement of the pore size distribution by the mercury intrusion method and the analysis by the Raman spectroscopy according to the procedure described above.
  • Tables 1 to 4 The evaluation test and analysis results are shown in Tables 1 to 4 below.
  • Table 1 also shows the weight C1 of the first carbon material, the weight C2 of the second carbon material, and their ratio C1 / C2 for each example.
  • Table 3 also shows the conditions of the preparation method of the positive electrode paint for each example. " ⁇ " indicates that the process was performed in preparation of the positive electrode paint, and " ⁇ ” indicates that the process was not performed in preparation of the positive electrode paint.
  • the solid kneading was performed, but since it was performed under more severe conditions than the conditions of the solid kneading of the other examples, it is set as “ ⁇ ”.
  • Table 3 describes the positive electrode active material and the negative electrode active material used in each example.
  • Examples 1-2 and 9-1 are examples in which the first carbon material is changed from Example 1-1. From the results shown in Table 4, although the first carbon material is different, the positive electrode produced in these examples realizes a non-aqueous electrolyte battery which can exhibit excellent output performance as in Example 1-1. I understand that I was able to do it.
  • Examples 1-3 to 1-7 are examples in which the second carbon material is changed from Example 1-1. From the results shown in Table 4, although the second carbon material is different, the positive electrode produced in these examples realizes a non-aqueous electrolyte battery which can exhibit excellent output performance as in Example 1-1. I understand that I was able to do it.
  • Examples 1-8 and 1-9 are examples in which the weight ratio C1 / C2 is changed from Example 1-1. From the comparison of these results, the results shown in Table 4 indicate that the positive electrodes produced in these examples show excellent output performance as in Example 1-1 although the weight ratio C1 / C2 is different. It can be seen that a non-aqueous electrolyte battery was realized.
  • Examples 1-10 to 1-13, 2-1, 3-1, 4-1, and 5-1 are examples in which the positive electrode active material is changed from Example 1-1. From the results shown in Table 4, although the positive electrode prepared in these examples was different in the positive electrode active material, it was possible to realize a non-aqueous electrolyte battery capable of exhibiting excellent output performance as in Example 1-1. I understand that. In Examples 2-1, 3-1, and 4-1, the strength ratio G 1 / D 1 and the strength ratio G 2 / of the first carbon material and the second carbon material contained in each non-aqueous electrolyte battery D 2 was different from those of Example 1-1. These are considered to be due to the difference in particle size and particle state.
  • Examples 6-1, 7-1 and 8-1 are examples in which the negative electrode is changed from Example 1-1. From the results shown in Table 4, it can be seen that, by using the positive electrode manufactured in Example 1-1, a non-aqueous electrolyte battery capable of exhibiting excellent output performance regardless of the composition of the negative electrode was realized.
  • the positive electrodes of the non-aqueous electrolyte batteries of Comparative Example 1-1 which did not perform the solid mixing, Comparative Example 1-14 that did not perform the shearing with the bead mill, and Comparative Example 1-15 that did not perform the shearing with the jet mill had a ratio P1 / P2 was 8 or more, and ratio S1 / S2 was 10 or more. Therefore, in the positive electrodes of Comparative Examples 1-1, 1-14, and 1-15, it is considered that the conductive aid was not uniformly dispersed in the positive electrode mixture layer. It is considered that this is the reason why the output characteristics of the nonaqueous electrolyte batteries of Comparative Examples 1-1, 1-14 and 1-15 are poor.
  • the ratio P1 / P2 was less than 2 and the ratio S1 / S2 was less than 3.
  • Comparative Example 1-2 since the pre-dispersion was not performed, it is considered that the first carbon material and the second carbon material were not properly mixed. Therefore, it is considered that the second carbon material becomes too fine by hard kneading, and many pores having a small pore diameter are generated. Further, in Comparative Example 1-3, it is considered that the shearing force was too strong at the time of solid mixing, and as a result, many pores with a small pore diameter were generated.
  • Comparative Examples 1-1 to 1-3, 1-14, and 1-15 were the same in that the same materials as in Example 1-1 were used, the manufacturing method was changed from Example 1-1. It is an example. From the comparison of the results of Example 1-1 with Comparative Examples 1-1 to 1-3, 1-14, and 1-15, the ratio P1 when the manufacturing method is different even if the positive electrode is manufactured using the same material It can be seen that the values of / P2 and the ratio S1 / S2 are different, and the difference in these ratios causes differences in output performance.
  • the positive electrodes of the nonaqueous electrolyte batteries of Comparative Examples 1-4 to 1-6 had a ratio P1 / P2 of less than 2 and a ratio S1 / S2 of less than 3.
  • Comparative Example 1-4 it is considered that the first carbon material has broken down during firming. Therefore, it is considered that the first carbon material can not sufficiently protect the second carbon material and the second carbon material is also broken during the solid kneading.
  • Comparative Example 1-6 since the amount of the first carbon material was too small, the first carbon material can not sufficiently protect the second carbon material during the hard mixing, and the second carbon material It is thought that it has collapsed.
  • the ratio P1 / P2 was 8 or more and the ratio S1 / S2 was 10 or more.
  • Comparative Example 1-7 it is considered that a sufficient shearing force was not applied to the second carbon material at the time of firming, because the amount of the first carbon material was too large. As a result, it is considered that the second carbon material was not sufficiently dispersed in the positive electrode paint prepared in Comparative Example 1-7. It is considered that in the positive electrode composite material layer of the positive electrode of Comparative Example 1-7 using such a positive electrode paint, the dispersed state of the conductive additive was bad. It is considered that this is the reason why the output characteristics of the nonaqueous electrolyte battery of Comparative Example 1-7 are poor.
  • Comparative Example 1-8 it is considered that the amount of the second carbon material was too small. As a result, it is considered that in the positive electrode mixture layer produced the positive electrode paint prepared in Comparative Example 1-8, the voids were too large and the conductive path could not be formed sufficiently. It is considered that this is the reason why the output characteristics of the nonaqueous electrolyte battery of Comparative Example 1-8 were poor.
  • the positive electrode of the nonaqueous electrolyte battery of Comparative Example 1-9 had a ratio P1 / P2 of less than 2 and a ratio S1 / S2 of less than 3.
  • the amount of the second carbon material is considered to be too large.
  • the number of voids was too small, and a path through which Li ions could not be sufficiently formed. It is considered that this is the reason why the output characteristics of the non-aqueous electrolyte battery of Comparative Example 1-9 were poor.
  • Comparative Examples 1-4 to 1-9 are examples in which the kind of the conductive auxiliary and / or the mixing ratio (weight ratio) in the pre-dispersion are changed from Example 1-1. From the comparison of the results of Example 1-1 and Comparative Examples 1-4 to 1-9, the ratio P1 / P2 and the ratio S1 / 1 when the materials and / or amounts are different even if the dispersion method in preparing the positive electrode paint is the same It can be seen that the values of S2 are different, and differences in these ratios lead to differences in output performance.
  • Example 1-10 and Comparative Example 1-10 A set of Example 1-10 and Comparative Example 1-10, a set of Example 1-11 and Comparative Example 1-11, a set of Example 1-12 and Comparative Example 1-12, Example 1-13 and Comparative Example 1-13, Example 2-1 and Comparative Example 2-1, Example 3-1 and Comparative Example 3-2, and Example 4-1 and Comparative Example 4-2. From the comparison of the respective results, it can be seen that the same tendency as the relationship of the set of Example 1-1 and Comparative Example 1-4 can be seen even when the positive electrode active material is different.
  • Example 5-1 and Comparative Example 5-1 a set of Example 5-1 and Comparative Example 5-1, a set of Example 6-1 and Comparative Example 6-1, a set of Example 7-1 and Comparative Example 7-1, and Example 8-1
  • the set of Comparative Example 8-1 is the same as that of Example 1-1 although the negative electrode used in the example and the comparative example is the same, but the positive electrode used in each example is
  • the positive electrode used in each of the comparative examples is a set produced in the same procedure as in Comparative Example 1-4. From the results shown in Table 4, it can be seen that in these groups, the non-aqueous electrolyte battery of the example exhibited better output performance than the non-aqueous electrolyte battery of the comparative example.
  • an electrode includes an electrode mixture layer containing an active material and a conductive aid.
  • the electrode mixture layer satisfies a ratio P1 / P2 within the range of 2 to less than 8 and a ratio S1 / S2 within the range of 3 to less than 10 in the log differential pore volume distribution by mercury porosimetry.
  • the conductive aid is sufficiently uniformly dispersed in the electrode mixture layer, the conductive aid sufficiently fills the voids between the active materials, and the diffusion of Li ions is inhibited. There are few pores passing through. Therefore, this electrode can realize a non-aqueous electrolyte battery capable of exhibiting excellent output performance.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Composite Materials (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

Selon un mode de réalisation, la présente invention concerne une électrode comprenant une couche de mélange d'électrode qui contient un matériau actif et un adjuvant conducteur. La couche de mélange d'électrode, dans une distribution du volume poreux différentiel logarithmique obtenue par intrusion de mercure, satisfait un rapport P1/P2 compris dans une plage allant d'au moins 2 à moins de 8, et un rapport S1/S2 compris dans une plage allant d'au moins 3 à moins de 10. P1 est une valeur du volume poreux différentiel logarithmique maximal dans une plage de diamètre de pore de 0,1 à 1 µm dans la distribution du volume poreux différentiel logarithmique de la couche de mélange d'électrode. P2 est une valeur du volume poreux différentiel logarithmique pour un diamètre de pore de 0,03 µm dans la distribution du volume poreux différentiel logarithmique de la couche de mélange d'électrode. S1 est une valeur intégrée dans une plage de diamètre de pore de 0,1 à 1 µm dans la distribution du volume poreux différentiel logarithmique de la couche de mélange d'électrode. S2 est une valeur intégrée dans une plage de diamètre de pore allant de plus de 0 µm à moins de 0,1 µm dans la distribution du volume poreux différentiel logarithmique de la couche de mélange d'électrode.
PCT/JP2017/033336 2017-09-14 2017-09-14 Électrode et pile à électrolyte non aqueux WO2019053861A1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP2019541582A JP6952784B2 (ja) 2017-09-14 2017-09-14 電極及び非水電解質電池
EP17924977.6A EP3683865B1 (fr) 2017-09-14 2017-09-14 Électrode et pile à électrolyte non aqueux
PCT/JP2017/033336 WO2019053861A1 (fr) 2017-09-14 2017-09-14 Électrode et pile à électrolyte non aqueux
CN201780094329.0A CN111052455B (zh) 2017-09-14 2017-09-14 电极及非水电解质电池
US16/806,005 US11967720B2 (en) 2017-09-14 2020-03-02 Electrode and nonaqueous electrolyte battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2017/033336 WO2019053861A1 (fr) 2017-09-14 2017-09-14 Électrode et pile à électrolyte non aqueux

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US16/806,005 Continuation US11967720B2 (en) 2017-09-14 2020-03-02 Electrode and nonaqueous electrolyte battery

Publications (1)

Publication Number Publication Date
WO2019053861A1 true WO2019053861A1 (fr) 2019-03-21

Family

ID=65723930

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2017/033336 WO2019053861A1 (fr) 2017-09-14 2017-09-14 Électrode et pile à électrolyte non aqueux

Country Status (5)

Country Link
US (1) US11967720B2 (fr)
EP (1) EP3683865B1 (fr)
JP (1) JP6952784B2 (fr)
CN (1) CN111052455B (fr)
WO (1) WO2019053861A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021057142A (ja) * 2019-09-27 2021-04-08 マクセルホールディングス株式会社 全固体電池用正極および全固体電池

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06132032A (ja) 1992-03-31 1994-05-13 Kuraray Co Ltd 非水電解液電池
JP2000182617A (ja) 1998-12-16 2000-06-30 Nkk Corp リチウム二次電池電極用炭素材料およびその製造方法およびリチウム二次電池
JP2001283831A (ja) * 2000-04-04 2001-10-12 Matsushita Electric Ind Co Ltd 非水電解質二次電池とその正極およびその正極の製造方法
JP2004134304A (ja) * 2002-10-11 2004-04-30 Hitachi Maxell Ltd 非水二次電池および正極塗料製造方法
WO2012111813A1 (fr) * 2011-02-18 2012-08-23 株式会社 東芝 Pôle positif, batterie électrolytique non aqueuse et bloc de batterie
JP2012209161A (ja) * 2011-03-30 2012-10-25 Toyota Central R&D Labs Inc リチウム二次電池
JP2012243463A (ja) 2011-05-17 2012-12-10 Hitachi Vehicle Energy Ltd 非水電解質二次電池
JP2014194927A (ja) * 2013-02-26 2014-10-09 Toyo Ink Sc Holdings Co Ltd 合材スラリーおよびその製造方法とそれを用いた電極、電池
JP2015084323A (ja) 2013-09-18 2015-04-30 株式会社東芝 非水電解質電池
JP2016033851A (ja) 2014-07-30 2016-03-10 株式会社東芝 複合体、複合体の製造方法、非水電解質電池用活物質材料、及び非水電解質電池
JP2016068258A (ja) 2014-09-26 2016-05-09 株式会社トッパン・コスモ 防湿シート

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4507284B2 (ja) 1997-03-11 2010-07-21 パナソニック株式会社 非水電解液二次電池
JP2001068093A (ja) * 1999-08-25 2001-03-16 Mitsubishi Cable Ind Ltd 正極活物質組成物およびそれを用いたリチウムイオン二次電池
JP2001167767A (ja) 1999-12-07 2001-06-22 Sony Corp 非水電解液２次電池
KR102297569B1 (ko) * 2005-10-20 2021-09-02 미쯔비시 케미컬 주식회사 리튬 2 차 전지 및 그것에 사용하는 비수계 전해액
KR101367613B1 (ko) * 2007-02-16 2014-02-27 나믹스 코포레이션 리튬이온 2 차 전지, 및 그 제조 방법
KR102270513B1 (ko) * 2014-08-05 2021-06-30 삼성에스디아이 주식회사 리튬 이차 전지용 양극 조성물, 그리고 이를 포함하는 리튬 이차 전지용 양극 및 리튬 이차 전지
JPWO2016068258A1 (ja) 2014-10-29 2017-06-29 株式会社東芝 正極及び非水電解質電池
JP6455708B2 (ja) * 2014-12-26 2019-01-23 トヨタ自動車株式会社 非水電解液二次電池およびその製造方法
JP6383326B2 (ja) * 2015-06-05 2018-08-29 プライムアースＥｖエナジー株式会社 非水電解液二次電池および非水電解液二次電池の正極活物質
JP6538500B2 (ja) * 2015-09-16 2019-07-03 株式会社東芝 非水電解質電池、電池パック、及び車
US11145900B2 (en) * 2016-02-12 2021-10-12 Samsung Sdi Co., Ltd. Lithium battery
JPWO2018139493A1 (ja) * 2017-01-24 2019-11-07 株式会社東芝 電極体、電極群、二次電池、電池モジュール及び車両

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06132032A (ja) 1992-03-31 1994-05-13 Kuraray Co Ltd 非水電解液電池
JP2000182617A (ja) 1998-12-16 2000-06-30 Nkk Corp リチウム二次電池電極用炭素材料およびその製造方法およびリチウム二次電池
JP2001283831A (ja) * 2000-04-04 2001-10-12 Matsushita Electric Ind Co Ltd 非水電解質二次電池とその正極およびその正極の製造方法
JP2004134304A (ja) * 2002-10-11 2004-04-30 Hitachi Maxell Ltd 非水二次電池および正極塗料製造方法
WO2012111813A1 (fr) * 2011-02-18 2012-08-23 株式会社 東芝 Pôle positif, batterie électrolytique non aqueuse et bloc de batterie
JP2012209161A (ja) * 2011-03-30 2012-10-25 Toyota Central R&D Labs Inc リチウム二次電池
JP2012243463A (ja) 2011-05-17 2012-12-10 Hitachi Vehicle Energy Ltd 非水電解質二次電池
JP2014194927A (ja) * 2013-02-26 2014-10-09 Toyo Ink Sc Holdings Co Ltd 合材スラリーおよびその製造方法とそれを用いた電極、電池
JP2015084323A (ja) 2013-09-18 2015-04-30 株式会社東芝 非水電解質電池
JP2016033851A (ja) 2014-07-30 2016-03-10 株式会社東芝 複合体、複合体の製造方法、非水電解質電池用活物質材料、及び非水電解質電池
JP2016068258A (ja) 2014-09-26 2016-05-09 株式会社トッパン・コスモ 防湿シート

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
"Measuring Methods of Powder Properties and Characteristics", 1973, ASAKURA PUBLISHING CO., LTD., pages: 257 - 259
JINBO GENJI ET AL.: "Handbook of Particles", 1991, ASAKURA PUBLISHING CO., LTD., pages: 151 - 152

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021057142A (ja) * 2019-09-27 2021-04-08 マクセルホールディングス株式会社 全固体電池用正極および全固体電池
JP7267163B2 (ja) 2019-09-27 2023-05-01 マクセル株式会社 全固体電池用正極および全固体電池

Also Published As

Publication number Publication date
EP3683865A1 (fr) 2020-07-22
US11967720B2 (en) 2024-04-23
CN111052455A (zh) 2020-04-21
JP6952784B2 (ja) 2021-10-20
EP3683865B1 (fr) 2023-09-06
CN111052455B (zh) 2023-05-23
EP3683865A4 (fr) 2021-04-21
US20200203730A1 (en) 2020-06-25
JPWO2019053861A1 (ja) 2020-06-18

Similar Documents

Publication Publication Date Title
US10418627B2 (en) Negative electrode active material for non-aqueous electrolyte secondary battery, non-aqueous electrolyte secondary battery, and method of producing negative electrode material for non-aqueous electrolyte secondary battery
EP1657767B1 (fr) Batterie secondaire et procede de fabrication de ladite batterie
EP3104440B1 (fr) Matériau actif d'électrode négative pour matériau d'électrode négative d'une batterie rechargeable à électrolyte non aqueux, électrode négative pour une batterie rechargeable à électrolyte non aqueux et batterie rechargeable à électrolyte non aqueux
US8178238B2 (en) Positive-electrode active material for lithium-ion secondary battery, positive electrode, manufacturing method thereof, and lithium-ion secondary battery
KR102343726B1 (ko) 비수전해질 이차 전지용 부극재 및 그의 제조 방법, 및 비수전해질 이차 전지용 부극 활물질층, 비수전해질 이차 전지용 부극, 비수전해질 이차 전지
EP3404751B1 (fr) Électode positive
JP7135269B2 (ja) 非水系電解質二次電池用正極活物質とその製造方法、非水系電解質二次電池用正極合材ペーストおよび非水系電解質二次電池
WO2022050251A1 (fr) Mélange d'électrodes pour batteries secondaires, feuille de mélange d'électrodes pour batteries secondaires, son procédé de production et batterie secondaire
WO2011016222A1 (fr) Pile secondaire à électrolyte non aqueux
WO2018030176A1 (fr) Batterie auxiliaire à électrolyte non aqueux
WO2015140907A1 (fr) Matériau actif pour accumulateurs à électrolyte non aqueux, électrode pour accumulateurs à électrolyte non aqueux, accumulateur à électrolyte non aqueux, bloc-batterie et procédé de production de matériau actif pour accumulateurs à électrolyte non aqueux
JP2022121546A (ja) 非水系電解液を使用する二次電池用電極の製造方法及び非水系電解液を使用する二次電池電極用結着剤
JP2018092707A (ja) 正極板の製造方法及び非水電解質二次電池の製造方法、並びに非水電解質二次電池
JP2018097961A (ja) リチウムイオン二次電池用正極及びリチウムイオン二次電池
JP2016051504A (ja) 非水系二次電池用正極活物質、非水系二次電池用正極、非水系二次電池及び車載用非水系二次電池モジュール
JP2007080583A (ja) 二次電池用電極と二次電池
JP7040832B1 (ja) リチウムイオン二次電池用負極活物質、その製造方法、及びリチウムイオン二次電池用負極電極
JP2024127969A (ja) 正極活物質、正極及びこれを含むリチウム二次電池
WO2017085907A1 (fr) Matière active d'électrode négative, électrode négative, batterie secondaire au lithium-ion ainsi que procédé de fabrication de celle-ci, et procédé de fabrication de matériau d'électrode négative pour batterie secondaire à électrolyte non aqueux
WO2023166869A1 (fr) Matériau actif d'électrode négative de batterie secondaire lithium-ion, procédé de production associé, et électrode négative de batterie secondaire lithium-ion
US11967720B2 (en) Electrode and nonaqueous electrolyte battery
US10211456B2 (en) Positive electrode active material for lithium ion secondary battery, and lithium ion secondary battery positive electrode and lithium ion secondary battery using the same
JP6607388B2 (ja) リチウムイオン二次電池用正極及びその製造方法
WO2018021480A1 (fr) Substance active d'électrode positive pour batteries secondaires au lithium-ion, électrode positive pour batteries secondaires au lithium-ion, et batterie secondaire au lithium-ion l'utilisant
WO2016068258A1 (fr) Électrode positive et batterie à électrolyte non aqueux

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 17924977

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2019541582

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2017924977

Country of ref document: EP

Effective date: 20200414